CN101333038A - Anaerobic dynamic film bio sewage treating process - Google Patents
Anaerobic dynamic film bio sewage treating process Download PDFInfo
- Publication number
- CN101333038A CN101333038A CNA2007100429303A CN200710042930A CN101333038A CN 101333038 A CN101333038 A CN 101333038A CN A2007100429303 A CNA2007100429303 A CN A2007100429303A CN 200710042930 A CN200710042930 A CN 200710042930A CN 101333038 A CN101333038 A CN 101333038A
- Authority
- CN
- China
- Prior art keywords
- sewage
- anaerobic
- dynamic membrane
- dynamic
- treatment
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- Y02W10/12—
Abstract
The invention discloses an anaerobic dynamic membrane biological sewage treatment technique and relates to the technology for treating anaerobic domestic sewage and industrial organic wastewater, the property of which is similar to that of domestic sewage, in particular relates to a method for treating anaerobic sewage by adopting dynamic membrane technology. The technique of the invention consists of an anaerobic bioreactor (tank) and a dynamic membrane component; the dynamic membrane component is arranged in the anaerobic bioreactor (tank). During sewage treatment, sewage firstly enters the anaerobic bioreactor (tank) for treatment, part of organic matter in the sewage can be decomposed by anaerobic activated sludge, and then the organic matter in the sewage is degraded and treated with solid-liquid separation by the biomembrane growing on the dynamic membrane component and is drained after being separated by the dynamic membrane component. The technique of the invention has the advantages of comparatively high treatment efficiency, low energy consumption, low construction investment, convenient operation and management and high social and economic benefits.
Description
Technical field
Anaerobic dynamic film bio sewage treating process relates to the similar industrial organic waste water treatment technology of anoxybiosis sewage disposal and character and sanitary sewage, relates in particular to the method that Dynamic membrane is carried out the anaerobism sewage disposal of using.
Background technology
In recent years, China's total amount of sewage discharge increases year by year, and wherein the city domestic sewage quantity discharged is with average annual 5% speed increase, according to statistics, 2005, national sanitary sewage quantity discharged was 281.4 hundred million tons, wherein the quantity discharged of chemical oxygen demand (COD) is 859.4 ten thousand tons, and the ammonia nitrogen quantity discharged is 97.3 ten thousand tons.And the centralized treatment rate of National urban sanitary sewage only is 29.44%, and a large amount of sanitary sewages directly discharge, and cause more and more serious environmental pollution problem.China concentrates about 80% employing activated sludge process in the sewage treatment process, comprises traditional activated sludge process, AO method, A
2O method, SBR method, AB method etc. are that the modern sewage of main flow technology focuses on technology with the activated sludge process, though treatment effect is relatively good, but exist initial outlay big, need lay shortcomings such as huge municipal sewage pipe network, operation and handling cost height, generally can only be applied to economic relatively advanced large and medium-sized city at present, and be restricted for the application of the middle samll cities and towns of economically underdeveloped area.
In addition, with regard to wastewater processing technology, with respect to aerobic treatment technology, Anaerobic Microbiological Treatment Technology has following characteristics: (1) construction, operation and simple to operate, and the expense of capital construction and operation is low; (2) energy requirement is low, save energy; (3) according to the requirement of water treatment, the scale of water treatment is changeable, makes that disperseing to carry out water treatment becomes possibility, and can reduce investment outlay greatly; (4) generation of the excess sludge of anaerobic treatment is few, good stability, and follow-up water treatment is easy.In recent years, the application of anaerobism film-bioreactor attracts much attention, compares with the anaerobic reactor of routine, and the anaerobism film-bioreactor has the volumetric loading height, floor space is little, effluent quality good and HRT and advantages such as SRT can separate fully.The decline of membrane flux is serious, film cleans inconvenient, the too high shortcoming of film Costco Wholesale but the anaerobism film-bioreactor also exists, and is difficult to large-scale application.
In aerobic sewage treatment process, at traditional micro-filtration or ultra-filtration membrane cost than higher shortcoming, the dynamic film bio treatment technology of wide-aperture material substitution conventional film has appearred utilizing, Chinese scholars has been carried out a lot of research to it, and YoshiakiKiso is applied to intermittent aeration device and A with the bolting silk Dynamic Membrane
2In the O technology, the TN clearance can reach 80% (Wastewatertreatment performance of a filtration bio-reactor equipped with a mesh as a fiter material.WaterResearch, 2000,34 (17): 4143-4150); Huang Xia (use Dynamic Membrane bioreactor mixed solution is carried out filtering method and device patent of invention publication number CN 1363526A) is processed into filter assemblies with common porous material, and bioreactor mixed solution is carried out filtering separation; Model refined (synergistic sewage water treatment method of dynamic biological film and activated sludge process and device patent of invention publication number CN 1490259A) is used the active sludge and the dynamic biomembranous synergy that suspend sewage is handled; Fan Yaobo (split-type tube type dynamic membrane bioreactor patent of invention publication number CN 1785841A) adopts split-type tube type dynamic membrane to dispose of sewage, and has obtained reasonable treatment effect.But, existing Dynamic Membrane technology all is applied in the aerobic activated sludge treatment process, the dynamic biological film of being mentioned is meant that also mixed solution is deposited on the membranaceous activated sludge layer in the basic unit when seeing through Dynamic Membrane basic unit, still needing in water treatment procedure provides the aeration oxygen supply and washes away the face cake layer, energy consumption is still than higher, and the water-in of device and the position of water outlet are provided with requirement, otherwise difficulty reaches ideal water treatment effect.
Adopt Dynamic membrane to carry out sewage disposal down about anaerobic state, do not appear in the newspapers as yet.
Summary of the invention
Deficiency at existing sewage disposal, the contriver is through research, proposed under anaerobic state, to utilize Dynamic membrane to carry out sewage disposal, biomembrance process separated with traditional Dynamic Membrane carry out combination, and water treatment efficiency is higher, operation energy consumption is low, the anaerobic dynamic film bio sewage treating process that construction investment is few.
Technology of the present invention is made up of anaerobic biological reactor (pond) and dynamic film component two portions, dynamic film component places anaerobic reactor (pond), dynamic film component is mainly by the porous material that is easy to biofilm development, as: bolting silk, filter cloth, wire cloth, also can adopt non-woven fabrics to be made into, select the dynamic film component of different apertures specification and material according to different influent quality situations for use.
When carrying out sewage disposal, sewage at first enters anaerobic reactor (pond) and handles, organism part in the sewage is degraded by anaerobic activated sludge, because dynamic film component mainly is made of porous material, in the water outlet operational process of ceaselessly intaking continuously, it can hold back the pollutent of some larger particles at first, make that the aperture on the dynamic film component can be stopped up gradually, the anaerobe film of on dynamic film component, also can growing simultaneously, the anaerobe film can be degraded to the organism in the sewage, and the continuous growth of anaerobe film forms gel coat with the accumulation of the pollutent that is trapped on the dynamic film component surface, cake layer, this layer forms in the water treatment operational process, and can be also referred to as Dynamic Membrane to the biomass rete that sewage filters with solid-liquid separation, Dynamic Membrane has good filtration and separation function, so just the anaerobe film is handled and be in the same place, make treated sewage through dynamic membrane filtering with the Dynamic Membrane separation and combination, water outlet after the separation has good water quality.In addition, pollutent and the microorganism flco held back by Dynamic Membrane pass through the certain hour decomposition and inversion, form certain density anaerobic activated sludge, the collaborative work in water treatment procedure of these anaerobic activated sludges and microbial film, pollutent in the sewage is removed, strengthen biological treatment effect, cleared up the suspension organic pollutant that is trapped.
Dynamic film component is through the successive water treatment, prolongation along with working time, the microbial film that is grown on the dynamic film component is more and more thicker, can influence the effect of water treatment, at this moment need dynamic film component is cleaned, for this reason, the biogas that can utilize anaerobic reactor to produce in water treatment procedure cleans the Dynamic Membrane on the dynamic film component and washes away, also can utilize the water outlet of anaerobic reactor to carry out back flushing, to keep certain microbial film thickness, guarantee the normal operation of anaerobic dynamic film bio sewage disposal.
Major advantage of the present invention is:
1. adopt Dynamic Membrane to carry out water treatment under anaerobic state, microbial film and Dynamic Membrane separation and combination are got up sewage is handled, realize separating fully of SRT and HRT, improved the quality of water treatment, the running cost of sewage disposal is effectively reduced.
2. adopt the wide aperture material as the Dynamic Membrane base material, as: bolting silk, filter cloth, wire cloth, or non-woven fabrics, draw materials easily, cheap, convenient operation and management, film cleans easily.
3. owing to adopt the anaerobic treatment mode, the methane recovery utilization that anaerobism can be produced has good society and economic benefit.
4. owing to adopt the anaerobic dynamic film processing mode, do not need oxygen consumption in whole water treatment procedure, energy consumption is low, water treatment effective.
Description of drawings
Fig. 1 is an embodiment of the invention process schematic representation.
Embodiment:
Example 1:
Adopt water technology of the present invention to carry out sewage disposal: dynamic film component 2 adopts non-woven fabrics to be made into, place anaerobic reactor 1, water inlet COD150～480mg/L, total hrt 3h, the water outlet of intaking continuously moves 150 days, pressure build-up is to 30KPa, utilized at interval biogas that 2 Dynamic Membrane on the dynamic film component is cleaned during this time in 40 days, water outlet COD＜100mg/L, the COD clearance is greater than 60%.
Example 2:
Adopt water technology of the present invention to carry out sewage disposal: dynamic film component 2 adopts the terylene bolting silk to be made into, place anaerobic reactor (pond), water inlet COD230～560mg/L, total hrt 4h, the water outlet of intaking continuously moves 135 days, pressure build-up is to 30KPa, utilized water outlet that 2 Dynamic Membrane on the dynamic film component are cleaned in 35 days at interval during this time, water outlet COD＜80mg/L, the COD clearance is greater than 70%.
Claims (2)
1. anaerobic dynamic film bio sewage treating process, it is characterized in that: dynamic film component (2) places anaerobic reactor (pond) (1), when carrying out sewage disposal, sewage at first enters in the anaerobic reactor (pond) 1, organism in sewage part is degraded by anaerobic activated sludge, and the organism in the sewage is grown in that anaerobe film on the dynamic film component (2) is degraded then, solid-liquid separation is after dynamic film component (2) water outlet.
2. anaerobic dynamic film bio sewage treating process according to claim 1 is characterized in that: dynamic film component (2) is made into by the porous material that is easy to biofilm development, also can adopt non-woven fabrics to be made into.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100429303A CN101333038B (en) | 2007-06-28 | 2007-06-28 | Anaerobic dynamic film bio sewage treating process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100429303A CN101333038B (en) | 2007-06-28 | 2007-06-28 | Anaerobic dynamic film bio sewage treating process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101333038A true CN101333038A (en) | 2008-12-31 |
| CN101333038B CN101333038B (en) | 2010-06-02 |
Family
ID=40195962
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007100429303A Active CN101333038B (en) | 2007-06-28 | 2007-06-28 | Anaerobic dynamic film bio sewage treating process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101333038B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101811802A (en) * | 2010-04-16 | 2010-08-25 | 同济大学 | online cleaning anaerobic micro-mesh reactor |
| CN102557349A (en) * | 2012-01-16 | 2012-07-11 | 同济大学 | Process and device of low energy consumption sewage treatment based on carbon source recovery |
| CN102557352A (en) * | 2012-02-03 | 2012-07-11 | 厦门神绿环保科技有限公司 | Method for treating organic wastewater through dynamic membrane anaerobic-aerobic integration |
| CN102874980A (en) * | 2012-09-24 | 2013-01-16 | 浙江工业大学 | Method for processing wastewater by utilizing combination of granular sludge and dynamic film |
| CN102951734A (en) * | 2012-11-26 | 2013-03-06 | 同济大学 | Wastewater treatment device with anaerobic dynamic membrane reactor |
| CN106145338A (en) * | 2016-08-08 | 2016-11-23 | 无锡合思环境技术有限公司 | A kind of Dynamic Membrane anaerobic reactor |
| CN106830520A (en) * | 2017-02-17 | 2017-06-13 | 上海恒霞环保设备有限公司 | Saprobia cleaning treatment system |
| CN114804347A (en) * | 2022-04-11 | 2022-07-29 | 重庆化工职业学院 | Anaerobic biological treatment process for sewage |
-
2007
- 2007-06-28 CN CN2007100429303A patent/CN101333038B/en active Active
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101811802A (en) * | 2010-04-16 | 2010-08-25 | 同济大学 | online cleaning anaerobic micro-mesh reactor |
| CN102557349A (en) * | 2012-01-16 | 2012-07-11 | 同济大学 | Process and device of low energy consumption sewage treatment based on carbon source recovery |
| CN102557352A (en) * | 2012-02-03 | 2012-07-11 | 厦门神绿环保科技有限公司 | Method for treating organic wastewater through dynamic membrane anaerobic-aerobic integration |
| CN102874980A (en) * | 2012-09-24 | 2013-01-16 | 浙江工业大学 | Method for processing wastewater by utilizing combination of granular sludge and dynamic film |
| CN102874980B (en) * | 2012-09-24 | 2014-03-26 | 浙江工业大学 | Method for processing wastewater by utilizing combination of granular sludge and dynamic film |
| CN102951734A (en) * | 2012-11-26 | 2013-03-06 | 同济大学 | Wastewater treatment device with anaerobic dynamic membrane reactor |
| CN106145338A (en) * | 2016-08-08 | 2016-11-23 | 无锡合思环境技术有限公司 | A kind of Dynamic Membrane anaerobic reactor |
| CN106830520A (en) * | 2017-02-17 | 2017-06-13 | 上海恒霞环保设备有限公司 | Saprobia cleaning treatment system |
| CN114804347A (en) * | 2022-04-11 | 2022-07-29 | 重庆化工职业学院 | Anaerobic biological treatment process for sewage |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101333038B (en) | 2010-06-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101333038B (en) | Anaerobic dynamic film bio sewage treating process | |
| CN102976566B (en) | System and method for treating high-concentration landfill leachate in aerobic composting site | |
| CN201258286Y (en) | Rubbish leachate handling arrangement | |
| CN101759324B (en) | Biological filter-ceramic membrane biological reactor device and water purifying application method thereof | |
| CN207405037U (en) | A kind of black and odorous water processing system of high-efficiency compact | |
| CN103496784B (en) | A kind of self-forming dynamic membrane bioreactor using aerobic particle mud | |
| CN106219752B (en) | A kind of control membrane fouling method during landfill leachate treatment | |
| WO2013063853A1 (en) | Wastewater disposal method using two-way oxygen supply horizontal-flow biofilm and equipment thereof | |
| CN201598221U (en) | Biofilter-ceramic membrane bioreactor | |
| CN201932988U (en) | Anaerobic/aerobic contact oxidation membrane bioreactor | |
| CN101643298A (en) | Organic wastewater treatment process containing membrane filtration element | |
| CN201106004Y (en) | Combined aerating biologic filtering pool | |
| CN101391833A (en) | Filter tank type membrane bioreactor | |
| CN203269735U (en) | Equipment for treating rubbish leachate by utilizing two-stage bioreactors | |
| CN214087881U (en) | Biological filtration sewage treatment system | |
| CN212610161U (en) | Full-flow treatment system for leachate of waste incineration plant | |
| CN205473253U (en) | Pharmacy sewage treatment plant | |
| CN210635851U (en) | Facultative MBR sewage treatment tank and equipment | |
| CN210796140U (en) | Domestic sewage treatment device | |
| CN211311017U (en) | Sewage advanced treatment equipment based on activated carbon technology | |
| CN210885506U (en) | Internal circulation high-efficiency denitrification biological denitrification filter tank | |
| CN207227239U (en) | A kind of garbage percolation liquid treating system | |
| CN202754840U (en) | Biological aerated filters in two-stage serial connection | |
| CN111908603A (en) | Novel anaerobic biological filter wastewater treatment equipment and wastewater treatment method thereof | |
| CN214781005U (en) | Draw-out type anaerobic gravity flow dynamic membrane biological reaction device with clamping groove |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANGHAI ZIZHENG ENVIRONMENTAL PROTECTION TECHNOLO Free format text: FORMER OWNER: TONGJI UNIVERSITY Effective date: 20140109 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 200092 YANGPU, SHANGHAI TO: 200086 HONGKOU, SHANGHAI |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20140109 Address after: 502-505 room 1619, 200086 Dalian Road, Shanghai Patentee after: Shanghai Zizheng Environment Protection Technology Co., Ltd. Address before: 200092 Shanghai City, Yangpu District Siping Road No. 1239 Patentee before: Tongji University |